Operational condition: Temperature, K = 313 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 | Mole fraction of Carbon dioxide (2) - Liquid mixture 1 |
---|---|
2130.00 | 0.3100 |
2760.00 | 0.3410 |
3450.00 | 0.5030 |
4140.00 | 0.5940 |
4830.00 | 0.6530 |
5170.00 | 0.6560 |
5520.00 | 0.6790 |
Operational condition: Temperature, K = 313 (Liquid mixture 2)
Pressure, kPa - Liquid mixture 2 | Mole fraction of Carbon dioxide (2) - Liquid mixture 2 |
---|---|
2130.00 | 0.1190 |
2760.00 | 0.1640 |
3450.00 | 0.2050 |
4140.00 | 0.2470 |
4830.00 | 0.3060 |
5170.00 | 0.3680 |
5520.00 | 0.4150 |
Operational condition: Temperature, K = 313 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 | Mole fraction of Hexane, tetradecafluoro- (1) - Liquid mixture 1 |
---|---|
2130.00 | 0.6900 |
2760.00 | 0.6560 |
3450.00 | 0.4950 |
4140.00 | 0.4020 |
4830.00 | 0.2710 |
5170.00 | 0.2150 |
5520.00 | 0.1610 |
Operational condition: Temperature, K = 313 (Liquid mixture 2)
Pressure, kPa - Liquid mixture 2 | Mole fraction of Hexane, tetradecafluoro- (1) - Liquid mixture 2 |
---|---|
2130.00 | 0.0220 |
2760.00 | 0.0160 |
3450.00 | 0.0100 |
4140.00 | 0.0090 |
4830.00 | 0.0170 |
5170.00 | 0.0190 |
5520.00 | 0.0270 |
Operational condition: Temperature, K = 313 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 | Mole fraction of Carbon dioxide (2) - Liquid mixture 1 |
---|---|
2130.00 | 0.3100 |
2760.00 | 0.3410 |
3450.00 | 0.5030 |
4140.00 | 0.5940 |
4830.00 | 0.6530 |
5170.00 | 0.6560 |
5520.00 | 0.6790 |
Operational condition: Temperature, K = 313 (Liquid mixture 2)
Pressure, kPa - Liquid mixture 2 | Mole fraction of Carbon dioxide (2) - Liquid mixture 2 |
---|---|
2130.00 | 0.1190 |
2760.00 | 0.1640 |
3450.00 | 0.2050 |
4140.00 | 0.2470 |
4830.00 | 0.3060 |
5170.00 | 0.3680 |
5520.00 | 0.4150 |
Operational condition: Temperature, K = 313 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 | Mole fraction of Hexane, tetradecafluoro- (1) - Liquid mixture 1 |
---|---|
2130.00 | 0.6900 |
2760.00 | 0.6560 |
3450.00 | 0.4950 |
4140.00 | 0.4020 |
4830.00 | 0.2710 |
5170.00 | 0.2150 |
5520.00 | 0.1610 |
Operational condition: Temperature, K = 313 (Liquid mixture 2)
Pressure, kPa - Liquid mixture 2 | Mole fraction of Hexane, tetradecafluoro- (1) - Liquid mixture 2 |
---|---|
2130.00 | 0.0220 |
2760.00 | 0.0160 |
3450.00 | 0.0100 |
4140.00 | 0.0090 |
4830.00 | 0.0170 |
5170.00 | 0.0190 |
5520.00 | 0.0270 |
Operational condition: Temperature, K = 313 (Liquid mixture 2)
Pressure, kPa - Liquid mixture 2 | Molar volume, m3/mol - Liquid mixture 2 |
---|---|
2130.00 | 0.0000 |
2760.00 | 0.0000 |
3450.00 | 0.0000 |
4140.00 | 0.0000 |
4830.00 | 0.0000 |
5170.00 | 0.0000 |
5520.00 | 0.0000 |
Operational condition: Temperature, K = 313 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 | Molar volume, m3/mol - Liquid mixture 1 |
---|---|
2130.00 | 0.0002 |
2760.00 | 0.0002 |
3450.00 | 0.0001 |
4140.00 | 0.0001 |
4830.00 | 0.0001 |
5170.00 | 0.0001 |
5520.00 | 0.0001 |
Operational condition: Temperature, K = 313 (Liquid mixture 2)
Pressure, kPa - Liquid mixture 2 | Molar volume, m3/mol - Liquid mixture 2 |
---|---|
2130.00 | 0.0000 |
2760.00 | 0.0000 |
3450.00 | 0.0000 |
4140.00 | 0.0000 |
4830.00 | 0.0000 |
5170.00 | 0.0000 |
5520.00 | 0.0000 |
Operational condition: Temperature, K = 313 (Liquid mixture 1)
Pressure, kPa - Liquid mixture 1 | Molar volume, m3/mol - Liquid mixture 1 |
---|---|
2130.00 | 0.0002 |
2760.00 | 0.0002 |
3450.00 | 0.0001 |
4140.00 | 0.0001 |
4830.00 | 0.0001 |
5170.00 | 0.0001 |
5520.00 | 0.0001 |